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  \section{Selective withdrawal in an isothermal stratifed fluid}
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 [References]: \\ 
Gelhar \& Mascolo, 1966\\
 R.C. Y. Koh, 1966 {\it J.  Fluid Mechanics}, {\bf 24}, pp. 555-575.\\
Brooks, N. H., \& Koh, R. C. Y., Selective withdrawal from density stratified reservoirs. {\it J Hydraulics ASCE}, HY4, July 1969. 1369-1400.\\
Ivey, G. N. \\
Monosmith, et. al. \\
 
Nuclear power plants are often located near a large lake    so that cold water can be withdrawn to cool the engines.  If the lake is thermally stratified so that there is apprciable temperature gradient vertically.  Cold water can be withdrawn from lake bottom,  and warm water from the power plant can be returned to the top of  lake. Due to the fact that stratification supresses vertical motion, water motion hence thermal mixing  should be limited  to a vertically thin layer  not far away from the intake. 

  In this section  we   treat    the   slow and steady  flow of an isothermal but    stratified fluid, due perhaps to salinity variation,   into a two- dimensional line sink.  The molecular diffusivity of salt is ignored. These simplifications permits a analytical solution which is easy to examine the physical implicaions. 
 

For a slow flow of a viscous fluid flowing in a vertically stratified fluid.
we expect, in light of Yih's theorem, that  the motion of the fluid  should  be confined within a thin layer.   

\subsection{Estimation of scales}
 
Governing equation  for continuity :
\be u_x+w_z=0 \ee
Ignoring mass diffusion, the incompressiblity condition reads
\be u \rho_x + w \rho_z = 0 \ee
\be \rho \lp uu_x + wu+z \rp = -p_x + \mu \lp u_{xx} + u_{zz} \rp \ee
\be \rho \lp uw_x + ww_z \rp = - p_z - \rho g + \mu \lp w_{xx} + w_{zz} \rp \ee
Anticipating a thin boundary layer due to vertical suppression, we introduce the following normalization. 
\be  u= Uu', ~w = \f{U\delta}{L} w' , ~ \rho = \rho_0 \rho' , ~x   =   Lx' , ~  z = \delta z' \ee then 
\be u'_x + w'_z= 0 \ee
\be u'\rho'_x + w'\rho'_z = 0 \ee 
\be \f{\rho_0U^2}{L} \lb \rho' \lp u'u'_x + w'u'_z \rp \rb = - \f{P}{L} \f{\p p'}{\p x'} + \f {\mu U}{\delta^2} \lp u'_{xx} \f{\delta^2}{L^2} + u'_{zz} \rp \ee
\be \f{\rho U^2}{L} \f{\delta}{L} \lb \rho' \lp u'w'_x + w'w'_z \rp \rb = - \f{P}{\delta} \f{\p p'}{\p z'} - \rho_0 g\rho' + \mu \f{U}{\delta^2} \f{\delta}{L} \lb w'_{xx} \f{\delta^2}{L^2} + w'_{zz} \rb \ee
Here $\delta $ is the boundary layer thickness, $ L\sim x $ is the horizontal length scale,   and $U $ is  the  horizontal velocity scale which must be of the order  $\sim Q/\delta$. 

After dividing  the $x,y$ momentum equations by
$\mu U\delta^2$,  and noting 
\be \f{\rho_0 U^2}{L} \,\, \f{\delta^2}{\mu U} = \lp \f{\rho_0 U \delta}{\mu} \rp \f{\delta}{L} \equiv R  \f{\delta}{L} \ee
we get
\be R  \f{\delta}{L} \lb \rho' \lp u'u'_x + w'w'_z \rp \rb = - \lp \f{P\delta}{\mu U} \f{\delta}{L} \rp p'_x + \lb u'_{xx} \lp \f{\delta}{L} \rp^2 + u'_{zz} \rb \ee
Assume
\be R= \f{\rho_0 U \delta}{\mu}=O(1), ~\mbox{and}~  \f{\delta}{L} \ll 1. \ee
We must have
\be \f{P\delta}{\mu U} \f{\delta}{L} = O(1)\ee so that  the viscous stress is forced by the pressure gradient. Thus we can take the pressure scale to be 
\be P = \mu \f{UL}{\delta^2} \label{press-scale}\ee
To the leading order the $x$ momentum equation is simply \be 0 = -p_x +\mu u_{zz} \ee

Now the $z$ momentum equation, 
\be \f{\rho_0 U^2}{L} \f{\delta}{L} \lb \rho' \lp u'w'_x + w'w'_z \rp \rb = - \f{P}{L} \f{1}{\delta /L} \f{\p p'}{\p z'} - \rho_0 g \rho' + \f{\mu U}{\delta^2} \f{\delta}{L} \lb w'_{xx} \f{\delta^2}{L^2} + w'_{zz} \rb . \ee
Dividing by $P/L$ and using (\ref{press-scale}), \be R \lp \f{\delta}{L} \rp \lb \rho' \lp w'w'_x + w'w'_z \rp \rb = - \f{1}{\lp \f{\delta}{L} \rp} \f{\p p'}{\p z} - \f{\rho_0 gL}{P} \rho' + \lp \f{\delta}{L} \rp \lb w'_{xx} \lp \f{\delta}{L} \rp^2 + w'_{zz} \rb \ee
i.e., 
\be R \lp \f{\delta}{L} \rp^2 \lb \rho' \lp w'w'_x + w'w'_z \rp \rb = - \f{\p p'}{\p z'} - \f{\rho_0 g \delta}{P} \rho' + \lp \f{\delta}{L} \rp^2 \lb w'_{xx} \lp \f{\delta}{L} \rp^2 + w'_{zz} \rb . \ee
Since gravity must be important, we must have
\be \f{\rho_0 g \delta}{P} = O(1),\label{buoyancy}\ee
The $z$ momentum equation reduces to 
\be 0= - \f{\p p}{\p z} - \rho g \ee
meaning that pressure is hydrostatic.


Now (\ref{buoyancy}) implies 
\be \f{\rho_0 g \delta^3}{\mu U L} =O(1) \ee
 since $Q  = O(U \delta ) $.
It follows that 
\be \f{\rho_0 g}{\mu Q} \f{\delta^4}{L} = O(1) \ee
i.e., \be  \delta^4 \sim \f{\mu Q L}{\rho_0 g} \ee
Since $L \sim x$, we have 
\be  \delta \sim\lp \f{\mu Qx}{\rho_0 g}\rp ^{1/4}\ee 
Thus by  a mere scale estimate, we not only achieved (confirmed)  a simplification, but also  conclude that the  boundary layer thickness increases with $x^{1/4}$.  

\subsection{Approximate equations}

We summarize the 
 the approximate equations stating continuity, 
\be u_x + w_z= 0 \label{Eq:42.15} \ee
incompressibility, 
\be u\rho_x + w \rho_z=0 \label{Eq:42.16} \ee
horizontal momentum balance,
\be 0 = -p_x + \mu \, u_{zz} \label{Eq:42.17} \ee
and vertical momentum balance
\be 0 = -p_z - \rho g . \label{Eq:42.18} \ee

 
Let the stream function $\psi$ be defined such that
\be u =  \psi_z, \qquad w = -\psi_x \label{streamfunction}\ee
 Equation (\ref{Eq:42.16}) means that in the direction of the local velocity, the density is constant. Thus the the density can only be a function of the stream function, i.e., 
\be  \rho = \rho (\psi ) \label{Eq:42.density}\ee
Let us check that (\ref{Eq:42.density}) implies (\ref{Eq:42.16}). Clearly
\[ \rho_x = \f{d\rho}{d\psi}   \psi_x, \quad  \rho_z = \f{d\rho}{d\psi}   \psi_z,\]
so that
\[ \f{d\rho}{d \psi} = 
\f{ \rho_x}{  \psi_x}=\f{\rho_z}{\psi_z} \]
Eq. (\ref{Eq:42.16}) follows by using  (\ref{streamfunction}). 

Eliminating $p$ between Eqn. (\ref{Eq:42.17}) and Eqn. (\ref{Eq:42.18}) we get \[ \mu \, u_{zzz} + g\rho_x = 0,  \]
which can be rewritten in terms of the $\psi$,  
\be \nu \, \psi_{zzzz} + \f{g}{\rho} \, \f{d\rho}{d \psi} \, \psi_x = 0 . \label{Eq:42.19'} \ee
Clearly this is a boundary layer equation. For a weakly stratifed fluid, we approximate  $\rho$ by a constant in the boundary layer. 

The boundary conditions are:
\be u,  \quad  z \to \pm \infty. \label{Eq:42.20a} \ee
which implies that 
\[  u_z, \, u_{zz}, u_{zzz}, ... \to 0, \quad z \to \pm \infty \]
It follows from Eqn. (\ref{Eq:42.19'}) that
\be  \psi_x = w \to 0 \qquad z \rightarrow \pm \infty   \label{Eq:42.20b} \ee
 if $d\rho/d\psi \neq 0$ as $z \to\pm \infty$.
Integrating Eqn. (\ref{Eq:42.15}) from $z = -\infty$ to $z = \infty$, and taking into account Eqn. (\ref{Eq:42.20b}), we get \[ \f{\p}{\p x} \, \int^\infty_{-\infty} \, u \, dz = 0 . \]
Therefore,
\be  \int^\infty_{-\infty} \, u \, dz = - Q \; \mbox{(const.)}  \label{Eq:42.21} \ee
where $Q$ denotes the steady discharge. 
 
 In terms of $\psi$, the boundary conditions Eqns. (\ref{Eq:42.20a}), (\ref{Eq:42.20b}) and the integral constraint Eqn. (\ref{Eq:42.21}) can be expressed as
\be  \psi_x, \, \psi_z, \, \psi_{zz} \rightarrow 0 \qquad (z \to \pm \infty)  \label{Eq:42.22} \ee
and
\be  \psi(x,\infty) - \psi(x,-\infty) = -Q . \label{Eq:42.23} \ee

{\bf Remark}:  Unlike the 2-D laminar jet problem discussed before,  the momentum flux rate is relatively unimportant in the present case of slow flow. 


 \subsection{Similarity solution for   linear stratification}
 In the present case $u<0$ hence $\psi$ increases as $z$ decreases. Therefore $ d \rho/d\psi$ and $d \rho/dz$ have  opposite signs.  For a stably stratified fluid, $\rho $ increases as $z$ decreases. Hence $d \rho/d \psi >0$. In the special case where 
\[ \f{g}{\rho}\f{d\rho}{d \psi} = \mbox{const.} \, \equiv \nu \, c > 0 \]
 (\ref{Eq:42.19'})   becomes linear
\be \psi_{zzzz} + c \psi_x = 0. \label{Eq:42.24} \ee
Let us look for a one-parameter transformation
\[x =\lambda^\alpha x^* ,z =\lambda^\beta z^* , \psi=\lambda^\gamma\psi^*   \]
such that  Eqns. (\ref{Eq:42.22}) - (\ref{Eq:42.24})  are  invariant.

Since Eqn. (\ref{Eq:42.22}) is homogeneous, it gives no information about the choice of $\alpha, \beta, \gamma$.  From Eqns. (\ref{Eq:42.23}) and (\ref{Eq:42.24}),   invariance of the boundary value problem requires that 
\[ \alpha = 4 \beta, \qquad \gamma = 0 . \]
Therefore,  a similarity solution can be found in the form
\be \f{\psi}{Q} = f(\eta), \qquad \eta = \lp \f{c}{x} \rp^{1/4} z \label{Eq:42.25} \ee

From  Eqn. (\ref{Eq:42.25}), it follows that
\be w = -\psi_x =  \f{Q}{4} \, \f{\eta}{x} \, f'(\eta) \label{vertical}\ee
\be u =  \psi_z =  \lp \f{c}{x} \rp^{1/4}Q \, f'(\eta), \label{horizontal}\ee
\be \psi_{zz} = \lp \f{c}{x} \rp^{1/2}Q \, f''(\eta) \ee
\be \psi_{zzzz} = \f{c}{x}  Q \, f''''(\eta) \ee
Eq(\ref{Eq:42.24})  then becomes
\be 4 \, f'''' -  \eta \, f' = 0 \label{Eq:42.26} \ee
and Eqns. (\ref{Eq:42.22}) and (\ref{Eq:42.23}) become
\be \eta \, f', \, f', \, f'' \rightarrow 0 \qquad (\eta \rightarrow \pm \infty) \label{Eq:42.27} \ee
\be f(\infty) - f(-\infty) = -1 . \label{Eq:42.28} \ee

{\bf Remarks}:
  
(i) Since $u(x, 0)$ must be finite, $f'(0)$ is finite. It follows that 
\[  w(x,0) = \left. -\f{Q}{4} \, \f{\eta}{x} \, f'(\eta) \right|_{\eta = 0} = 0 . \]
suggesting  that $w$ is odd in $\eta$ and antisymmetric  about $z = 0$, in the $x,z$ plane.  Hence $f(\eta)$ is also    anti-symmetric in $z$ about $z = 0$, i.e., $f(-\eta) = -f(\eta)$.    Eqn. (\ref{Eq:42.28}) may be repleced 
by
\be    f(\infty) = -1/2 \label{Eq:42.28'} \ee
It is always possible to take $f(0) = 0$, amounting to designating the axis as the streamline $\psi=0$.  

The anti-symmetry  of $w$ also implies symmetry of $u$ in $z$ about $ z= 0$. These properties are  the consequence of the assumption  that $d\rho/d \psi $ is constant and cannot be expected in general because of gravity. 

 

  (ii) The similarity transformation can also be derived heuristically by examining Eqns. (\ref{Eq:42.22}) - (\ref{Eq:42.24}).  Specifically,  Eqn. (\ref{Eq:42.24}) implies that
\[ \f{1}{\delta^4} \sim \f{1}{x},  \quad \mbox{thus}\quad   \delta \sim x^{1/4}  \]
where $\delta$ is the boundary layer thickness. Moreover, Eqn. (\ref{Eq:42.21}) gives $u \cdot \delta \sim O(1)$.  Therefore,
\[ u \sim \f{1}{\delta} \sim x^{1/4}, \quad \mbox{and} \quad  {\psi \sim u \delta \sim x^0} . \]
These results agree with (\ref{horizontal}). 

\subsection{Analytical Solution}

 Let
\be g(\eta) = f'(\eta) . \label{Eq:42.29} \ee
It follows from Eqn. (\ref{Eq:42.26}) that 
\be 4 \, g''' -  \eta \, g = 0 . \label{Eq:42.30} \ee
Furthermore, in view of Eqn. (\ref{Eq:42.27}), $g$ and its derivatives   vanish at $\eta = \pm \infty$.  Let us apply Fourier transform defined by 
\[ \hat{g}(k) = \f{1}{2\pi} \int^\infty_{-\infty} \, e^{-ik\eta} \, g(\eta) d\eta \, ; \]
Eqn. (\ref{Eq:42.30}) is then converted to
\[ -4 \, ik^3\hat{g} -   i \, \f{d\hat{g}}{dk} = 0 \]
The solution is 
\[
 \hat{g} (k) = A \, e^{-k^4} , \]
where $A$ is a coefficient. 

 Taking the inverse Fourier transform of $\hat{g}$, we get
\be g(\eta) = A \int^\infty_{-\infty} e^{-k^4 + ik\eta} \, dk = 2A \int^\infty_0 \, \cos \, k\eta \, e^{-k^4} \, dk. \label{Eq:42.31} \ee
It is readily seen from Eqn. (\ref{Eq:42.31}) that $g(-\eta) = g(\eta)$, confirming   the  earlier arguments on the symmetry of $u$ and $f'(\eta)$.

In view of Eqns. (\ref{Eq:42.28'}) and (\ref{Eq:42.29}), the constant $A$ must be chosen such that
\[ 2A \int^\infty_0 \, d\eta \, \int^\infty_0 \, dk \, \cos \, k\eta \, e^{-k^4} =-\f{1}{2} \]
It is shown in the Appendix that the double integral is $-\pi/2$ so that 
\[  A = -\f{1}{2\pi}. \]
In particular,
\[ g(0) = 2A \int^\infty_0 \, e^{-k^4} \, dk =  \f{-\sqrt{2}}{4\Gamma (3/4)} =  -0.2885 . \]
The integral in Eqn. (\ref{Eq:42.31}) may be evaluated numerically.  Alternatively,  Eqn. (\ref{Eq:42.30}) is solved numerically by  Chebyshev-polynomial method  for unbounded domains (as, for example, J.P. Boyd (1992), {\bf J. Comp. Phys.}, \underline{45}, 43-79).     Homework by Prof C. S. Wu,  1.63 class of 1995, now at U of Wisconsin, Madison)


From Figure \ref{fig:selwith-yang} ( Prof. T.S. Yang, National Cheng Kung University, Taiwan (1.63 Class of 1995)  it is seen that, away from the center line of the sink, there are regions in which $u > 0$.  Under the assumption that $c > 0$, we have, $\p \rho/\p y > 0$ so that locally the fluid may be  statically unstable. 
\setcounter{figure}{0}
 
\begin{figure}[h]
	\begin{center}
	 \includegraphics[scale=0.50]{dsf1}
	\end{center}
{Velocity profile of a 2D slow flow into a line sink in a density-stratified fluid. Calculations by G. D. Lee, 2002}  
	\label{fig:selwith-yang}
\end{figure}



  
\subsection*{Appendix: A double integral (Yang, 1995, Homework)}
 
Consider the double integral
\be  I(n)=\int^\infty_0 \,   dk \,e^{-k^n}\int^\infty_0  \, d\eta \, \cos \, k\eta \, \label{eq:doubleinetgral}\ee
Note that 
\[ \int_{-\infty}^\infty \delta(k) e^{ik\eta} \, dk = 1\]
By inverse transform we get the Fourier integral representation of the delta function:
\[ \delta(k) = \f{1}{2\pi}\int_{-\infty}^\infty   dk \,e^{-ik\eta}=\f{1}{\pi}\int_{0}^\infty   d\eta \,\cos k\eta \]
Now we use this result in (\ref{eq:doubleinetgral}) to get 
\be  I(n) =\pi \int_0^\infty \delta(k) e^{-k^n} dk = \f{\pi}{2}\label{Yang-int}\ee
It is interesting that the  result is independent of  $n$. Let us verify  (\ref{Yang-int}
) by   independent calculations for $n=1,2$:
 
\[ I(1) =\int^\infty_0 \,   dk \,e^{-k}\int^\infty_0  \, d\eta \, \cos \, k\eta \,  \]
Since 
\[  \int^\infty_0 \,   dk \,e^{-k} \cos \, k\eta \,  = \f{1}{1+\eta^2}\]
and 
\[ \int_0^\infty d\eta \f{1}{1+\eta^2}= \left.\tan^{-1}\eta \right|_0^\infty = \f{\pi}{2}\] 
(\ref{Yang-int}) is proven. 

\[ I(2)=\int^\infty_0 \,   dk \,e^{-k^2}\int^\infty_0  \, d\eta \, \cos \, k\eta \,  \]
Since 
\[  \int^\infty_0 \,   dk \,e^{-k^2} \cos \, k\eta \,  = \f{\sqrt{\pi}}{2}\, e^{-\eta^2/4}\]
and 
\[\f{ \sqrt{\pi}}{2}\int_0^\infty d\eta \,e^{-\eta^2/4}= \f{ \sqrt{\pi}}{\sqrt{2}}\int_0^\infty d\eta \,e^{-\eta^2}= \f{\pi}{2}\] 
(\ref{Yang-int}) is proven again. 

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